Page 551 - Elements of Chemical Reaction Engineering Ebook
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                               Chap. 8,  Questions and Problems                               52
                                      (a)  The reaction discussed in Problem P8-15 is to be carried wdt  in a single
                                          plug-flow  reactor  immersed  in  a  coolant  and  in  a  radial  flow  reactor
                                          immersed in the same coolant. The tubular flow reactor is 2 ft in diameter.
                                          The height of the radial flow reactor is  in. and the diameter of the inilet is
                                          1 in.  In  both  cases  the  coolant  temperature  is  100°C  and  the  werall
                                          heat-transfer coefficient is 2000 J/ m2 * h + "C . Plot conversion and ternper-
                                          atures as a function of reactor radius.
                                PS-19,  The zero-order exothermic liquid-phase reaction
                                                                  A-+B
                                       is carried out at 85°C in a jacketed 0.2-m3 CSTR. The coolant temperature in
                                       the rcacitor is 32°F. The heat transfer coefficient is  120 W/ m2  K . Determine
                                       the critilcal  value of  the heat-transfer area below  which  the reactor will  run
                                       away and explode [Chem. Eng., 91(10), 54.(1984)].
                                       Additional  information:
                                                        k  = 1.127 kmol/m3.min at4O"C
                                                        k  = 1.421 kmol/m3.min at 50°C
                                       The heat capacity of the solution is 4 J/g. The solution density is 0.90 kgi'dm3.
                                       The heat of reaction is ;SO0  J/g. The feed temperature is 40°C and the feed
                                       rate is 90 kg/min. MW of A = 90 g/mol.
                                PS-20B  The elementary reversible liquid-phase reaction
                                                               A-B
                                       takes place in a CSTR with a heat exchanger. Pure A enters the reactor.
                                       (a)  Derive an expression (or set of  expressions) to calculate G(T) as a fuilc-
                                          tion  of  heat  of  reaction, equilibrium constant,  temperature, and  so  on.
                                           Show a sample calculation for G(T) at T = 400 K.
                                       (b)  What are the steady-state temperatures? (Am.: 310, 377,418 K)
                                       (c)  Which steady states are locally stable?
                                       (a) What is the conversion corresponding to the upper steady state?
                                       (e)  Vary the ambient temperature T, and make SI plot of the reactor temperature
                                           as a function of T, , identifying the ignition and extinction temperatures.
                                       (f')  If  the heat  exchanger in  the reactor suddenly fails (Le.,  UA = 0), what
                                           would be the conversion and the reactor temperature wher. the new upper
                                           steady state is reached? (Ans.: 431 K)
                                       (g)  Write a question that requires critical thinking and then explain why your
                                           question requires critical thinking. [Hint: See Preface p.xx]
                                       (h)  What is the adiabatic blowout flow rate, u,, .
                                       (i)  Suppose that you want to operate at the lower steady state. What parameter
                                           values would you suggest to prevent runaway?
                                       Additional  information:
                                            UA = 3600 cal/min. K         EIR = 20,000 K
                                            Cp, = Cp, = 40 cal/mol* K    v- 10dm3
                                            A HRx = - 80,000 cal/mol A   uo = 1 dm3/min
                                            Keq = 100 at 400 K           FAo == 10 mol/min
                                            k  = 1 min-'  at 400 K
                                            Ambient temperature, T, = 37°C   Feed temperature, To = 37°C
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